Process and products of chinese kaolin

ABSTRACT

Disclosed are methods of processing Chinese kaolin involving providing Chinese kaolin having a desired powder size, delaminating the Chinese kaolin, pulverizing the delaminated Chinese kaolin at least two times, and heating the at least twice pulverized Chinese kaolin. Also disclosed are systems for automated processing of Chinese kaolin containing a pulverizer for pulverizing Chinese kaolin, a tester for testing and generating data of at least one parameter of the Chinese kaolin or at least one parameter of the pulverizer, a controller, operatively coupled to the pulverizer and the tester, for controlling operation of the pulverizer based on data received from the tester.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of and is a Divisional applicationof co-pending application Ser. No. 10/777,328 filed on Feb. 12, 2004,which is hereby incorporated by reference.

FIELD OF THE INVENTION

The present invention generally relates to processes and products thatare made using Chinese kaolin, also known as Shanxi kaolin. Inparticular, the present invention relates to pulverizing the kaolintwice before heat treatment or calcination.

BACKGROUND OF THE INVENTION

Kaolin is a fine usually white clay formed by the weathering ofaluminous minerals (as feldspar) and mainly consists of kaolinite.Kaolinite is commonly represented by one or more of the chemicalformulae Al₄Si₄O₁₀(OH)₈; Al₂O₃.2SiO₂.2H₂O; and/or Al₂Si₂O₅(OH)₄. Kaolinis one of the many industrial minerals mined today. Reserves are foundin Georgia (USA), Egypt, Brazil, United Kingdom, Queensland (Australia),Korea, and Ukraine.

The mining of many industrial minerals in China is rapidly increasing.Kaolin is among these industrial minerals. Kaolin deposits exist in theShanxi province of China. However, Shanxi kaolin may differ from kaolinfound in other parts of the world.

Generally speaking, kaolin from different countries, and even differentdeposits within the same country, differs in many respects due tovariations in a number of kaolinite properties. Examples of suchproperties include degree of crystallinity, particle size, particleshape, size and/or shape distribution. Variations in properties lead todifferences in performance of the resultant kaolin products. Forexample, crystallinity impacts resultant brightness, whiteness, opacity,gloss, and viscosity of the resultant products. Particle size, shape,and distribution impacts the smoothness, optical properties, and flowproperties of the resultant products.

The greatest demand for kaolin based products comes from the paperindustry, which uses them to coat and fill papers and boards. However,kaolin based products include paints, agricultural compositions,fiberglass products, polymer and rubber compositions, ceramicapplications, catalyst supports, pharmaceuticals, cosmetics and personalcare applications such as facial masks and body masks, electricalcomponents, adhesives, filter aids, and many more. Improved processingof kaolin and improved kaolin products are likely to provide improvedproducts that contain or employ kaolin.

SUMMARY OF THE INVENTION

The following presents a simplified summary of the invention in order toprovide a basic understanding of some aspects of the invention. Thissummary is not an extensive overview of the invention. It is intended toneither identify key or critical elements of the invention nor delineatethe scope of the invention. Rather, the sole purpose of this summary isto present some concepts of the invention in a simplified form as aprelude to the more detailed description that is presented hereinafter.

The present invention provides processes and products that are madeusing Chinese kaolin, also known as Shanxi kaolin, involving pulverizingthe kaolin twice before heat treatment. At least two distinctpulverization acts improves the quality of the heat treated kaolinincluding calcined kaolin that is produced.

One aspect of the invention relates to methods of processing Chinesekaolin involving providing Chinese kaolin having a desired particle sizedistribution, delaminating the Chinese kaolin, drying the delaminatedChinese kaolin, pulverizing the delaminated and dried Chinese kaolin atleast two times, and heating the at least twice pulverized Chinesekaolin.

Another aspect of the invention relates to systems for automatedprocessing of Chinese kaolin containing a pulverizer for pulverizingChinese kaolin, a tester for testing and generating data of at least oneparameter of the Chinese kaolin or at least one parameter of thepulverizer, a controller, operatively coupled to the pulverizer and thetester, for controlling operation of the pulverizer based on datareceived from the tester.

To the accomplishment of the foregoing and related ends, the inventioncomprises the features hereinafter fully described and particularlypointed out in the claims. The following description and the annexeddrawings set forth in detail certain illustrative aspects andimplementations of the invention. These are indicative, however, of buta few of the various ways in which the principles of the invention maybe employed. Other objects, advantages and novel features of theinvention will become apparent from the following detailed descriptionof the invention when considered in conjunction with the drawings.

BRIEF SUMMARY OF THE DRAWINGS

FIG. 1 is a flow diagram of one aspect of a system and method ofprocessing Chinese kaolin in accordance with the present invention.

FIG. 2 is a flow diagram of another aspect of a system and method ofprocessing Chinese kaolin in accordance with the present invention.

FIG. 3 is a schematic diagram of another aspect of a system forautomated processing of Chinese kaolin in accordance with the presentinvention.

FIG. 4 is a graphical illustration plotting the number of pre-heatingpulverization acts versus black glass scattering.

DETAILED DESCRIPTION OF THE INVENTION

The kaolin processed in accordance with the present invention containsat least some Chinese Kaolin. In other words, Chinese kaolin isprocessed in accordance with the present invention, or a mixture ofChinese kaolin and another clay substance such as Georgian kaolin (USA)is processed in accordance with the present invention. Chinese kaolin isdefined as kaolinite that is obtained from the country of China withborders defined in the year 2003. Chinese kaolin is sometimes referredto as Shanxi kaolin. It has been found that Chinese kaolin ischaracterized by one or more of several attributes, when compared tokaolin from Middle Georgia (USA): low titania content, low iron oxidecontent, a higher propensity to release alumina upon heating, high acidsolubility, and high carbon content.

Chinese kaolin mined from the Earth is subjected to preliminaryprocessing and/or beneficiation to facilitate transportation and/orstorage of the raw material. While crude kaolin can be subjected to oneor more of a number of preliminary processing acts, the Shanxi crudekaolin is initially crushed. Crushing reduces kaolin rock to gravel;that is, kaolin rock having diameters of less than about 10 cm indiameter. Crushers are made by the following manufacturers: Stedman,Svedala, Symons, Nordberg, Telsmith, Traylor, KVS, Allis-Chalmers,Jeffrey, Pennsylvania, American, SBM, and DFC. The particularpreliminary processing employed, if any, is not critical to the presentinvention.

Grinding involves processing crude kaolin to achieve a desired size.Grinding may be carried out by dry milling, dry ball milling, drygrinding, and the like. Grinding aids may be added to the kaolin tofacilitate grinding. When a desired powder size is achieved, subsequentdelamination is employed to achieve a desired particle size.

In one embodiment, grinding is performed to provide kaolin wherein atleast about 90% by weight of the kaolin has an equivalent sphericaldiameter of about 75 microns or less and from about 0.01% to about 90%by weight of the kaolin has an equivalent spherical diameter of about 2microns or less. In another embodiment, grinding is performed to providekaolin wherein at least about 90% by weight of the kaolin has anequivalent spherical diameter of about 60 microns or less and from about0.1% to about 50% by weight of the kaolin has an equivalent sphericaldiameter of about 2 microns or less. In yet another embodiment, grindingis performed to provide kaolin wherein at least about 90% by weight ofthe kaolin has an equivalent spherical diameter of about 45 microns orless and from about 1% to about 10% by weight of the kaolin has anequivalent spherical diameter of about 2 microns or less.

There are a number of methods and devices for measuring particle sizesin this range. For the purposes of this invention particle size isdetermined by conventional sedimentation techniques using Micromeretics,Inc.'s SEDIGRAPH® 5100 particle size analyzer. Particles are slurried inwater with a dispersant and pumped through the detector with agitationto disperse loose agglomerates.

Dry milling or grinding typically involves using energy inputs fromabout 5 horsepower hour per ton of dry kaolin to about 50 horsepowerhour per ton of kaolin. Grinding may be carried out using apparatus suchas a Raymond mill, a horizontal mill, a media mill such as a Pattersoncontinuous ball mill in which the grinding media comprises porcelain orstainless steel balls of less than 5 inches diameter. Grinding mills aremade by the following manufacturers: Raymond, Northwest, Denver,Allis-Chalmers, Marcy, Hardinge, KVS, Marion, and Traylor. Any type ofdry milling that achieves the desired particle size distribution can beemployed.

After the Chinese kaolin is processed so that it has a desired powdersize, it is subjected to delamination. Kaolin, in most cases, containsnaturally separated platy kaolin particles as well as “booklets”, whichcomprise stacks of kaolin platelets. These stacks are concentrated inparticles having a size of about 2 or more microns. Delamination ofthese booklets involves providing impact energy which is just sufficientto cleave apart the kaolin platelets that make up the booklets withoutfurther fracturing the kaolin platelets. In other words, delaminationalters or changes kaolin having a first structure to kaolin with asecond structure, different from the first structure. The resultingdelaminated particles are highly crystalline. In delamination, theincrease in the content of particles finer than about 2 micronsparticles is generally minimal.

Delamination can involve wet milling, slurry milling, wet grinding, andthe like. Such delamination processes involve the use of a grindingmedia, and water. Kaolin is combined with the water to form slurry andtransported, such as by pumping, through the delamination equipment thatcontain the media. Typically, the kaolin is delaminated at solids offrom about 5% to about 45% by weight.

Optionally, a clay dispersant and/or fluxing agent are also added to theslurry to provide additional fluidity to facilitate processing andhandling. Examples of clay dispersants include ammonia-baseddispersants, phosphate-based dispersants, sulfonate dispersants,carboxylic acid dispersants, and polymeric dispersants, such aspolyacrylate dispersants, as well as other organic dispersants employedin kaolin pigment processing. The amount of dispersant used in theslurry is typically from about 0.01% to about 1% based on the weight ofkaolin.

The grinding media is a relatively dense, hard particulate materialwhich does not substantially discolor the clay, or charge or leaveobjectionable residues in the ground clay. For example, the density ofthe grinding media is at least about 1.5. Examples of grinding mediainclude glass beads, alumina, zirconia, small ceramic balls or beads,coarse sand, plastic cylinders, stainless steel beads, beads or pelletsof nylon, styrene-divinyl benzene copolymer, polyethylene or other hardplastic, and the like.

The volume of beads to clay in the slurry is sufficient to effectdelamination. In one embodiment, the slurry of at least water, kaolin,and grinding media contains from about 10% to about 70% by volume ofgrinding media. In another embodiment, the slurry contains from about25% to about 50% by volume of grinding media.

An exemplary suitable vessel used for delamination contains verticalbaffles. Such a vessel can be equipped with an agitation systemcontaining multiple agitator elements attached to a vertical shaft. Thenumber and spacing of the agitators varies, but is selected for thespecific process conditions in order to impart the necessary combinedshear and percussive and frictional energy input necessary to overcomethe Van der Waals forces holding individual platelets in a stacked arrayor booklet. Energy input required for delamination varies due todifferences between specific kaolin crudes, process conditions, andequipment; typically, requiring 5 to 75 horsepower hour per ton ofkaolin charged to the delaminators.

The resultant slurry of delaminated kaolin contains more fine particlesof kaolin. In one embodiment, the resultant slurry of delaminated kaolincontains at least about 60% by weight of kaolin having an equivalentspherical diameter of about 2 microns or less. In another embodiment,the resultant slurry of delaminated kaolin contains at least about 80%by weight of kaolin having an equivalent spherical diameter of about 2microns or less. In yet another embodiment, the resultant slurry ofdelaminated kaolin contains at least about 90% by weight of kaolinhaving an equivalent spherical diameter of about 2 microns or less. Instill yet another embodiment, the resultant slurry of delaminated kaolincontains at least about 94% by weight of kaolin having an equivalentspherical diameter of about 2 microns or less.

Screening can be employed to remove the milling media, and optionally,can be employed to remove particles larger than 40 microns. Filtrationcan also be employed to effectively remove water prior to spray drying.The kaolin is optionally washed during this stage. Optionally,fractionation can be employed to separate the coarse particles. In thisconnection, a certrifuge may be used to perform the water separation.

After delamination, water is removed from the delaminated kaolin to drythe kaolin. The kaolin is dried by any suitable technique. Examples ofdrying kaolin include spray drying, flash drying, rotary drying, orother conglomeration techniques. These drying techniques are known inthe clay industry.

Drying the kaolin is performed to reduce the moisture level of thekaolin, in part, to facilitate subsequent heat treatments. In oneembodiment, after drying, the kaolin has a moisture level of less thanabout 5% by weight. In another embodiment, the kaolin has a moisturelevel of less than about 1.5% by weight. In yet another embodiment, thekaolin has a moisture level of less than about 1% by weight. In stillyet another embodiment, the kaolin has a moisture level of less thanabout 0.5% by weight.

Prior to heat treatment, such as calcinations, and generally after thecrude kaolin has a desired equivalent spherical diameter, the kaolin ispulverized in at least two separate acts (twice pulverized). Onepulverization treatment, or a pulverization treatment for longer thanusual time is not sufficient. At least two distinct pulverizationtreatments are performed on the kaolin ready for heat treatment. In oneembodiment, the kaolin is pulverized in at least three separate acts(thrice pulverized). In another embodiment, the kaolin is pulverized inat least five separate acts (four times pulverized). In yet anotherembodiment, the kaolin is pulverized in at least seven separate acts(five times pulverized). In still yet another embodiment, the kaolin ispulverized in at least nine separate acts (seven times pulverized).

The first pulverization is believed to break up any agglomerates thatmay be present. Such agglomerates may form during drying, changing theparticle size achieved by delamination. Chinese kaolin has a relativelyhigh amount of carbon therein. Although not wishing to be bound by anytheory, it is believed that the second pulverization act serves toexpose carbon from within the kaolin so that it may be consumed duringsubsequent heating. The at least two pulverization acts therefore servesto provide one or more of a certain particle size, a certain shape forthe kaolin particles, kaolin particles where carbon therein is exposed,and kaolin that undergoes desirable thermal structuring underapplication of heat.

The two or more pulverization acts provides kaolin wherein at leastabout 80% by weight has an average particle diameter of about 2 micronsor less. In another embodiment, the two or more pulverization actsprovides kaolin wherein at least about 90% by weight has an averageparticle diameter of about 2 microns or less. In yet another embodiment,the two or more pulverization acts provides kaolin wherein at leastabout 93% by weight has an average particle diameter of about 2 micronsor less. In still yet another embodiment, the two or more pulverizationacts provides kaolin wherein at least about 95% by weight has an averageparticle diameter of about 2 microns or less. Moreover, the two or morepulverization acts provides kaolin wherein at least about 60% by weighthas an average particle diameter of about 1 micron or less. In anotherembodiment, the two or more pulverization acts provides kaolin whereinat least about 70% by weight has an average particle diameter of about 1micron or less. In yet another embodiment, the two or more pulverizationacts provides kaolin wherein at least about 80% by weight has an averageparticle diameter of about 1 micron or less.

The two or more pulverization acts provides kaolin with a reduced bulkdensity. In one embodiment, the bulk density of the at least twicepulverized kaolin is at least about 25% less than the bulk density priorto the two or more pulverization acts. In another embodiment, the bulkdensity of the at least twice pulverized kaolin is at least about 40%less than the bulk density prior to the two or more pulverization acts.In yet another embodiment, the bulk density of the at least twicepulverized kaolin is at least about 50% less than the bulk density priorto the two or more pulverization acts.

General types of pulverizers that can be employed for pulverizinginclude Bowl, Hammer, Ball & Race type, IMP, Double Cone, Screen TypeRoller Mill, and Roller Mill. Pulverizing can be carried out in a highenergy impact mill, such as a Hurricane® mill; a Bauer hammer millavailable from C.E. Bauer Co. of Chicago, III; a Mikro Mill availablefrom Pulverization Machinery Company; a Mikro Sampimill available fromHosokawa Micron Powder Systems; or a Mikro-Pulverizer hammer mill alsoavailable from Hosokawa Micron Powder Systems. Other pulverizers aremade by the following manufacturers: Alpine, Williams, Raymond, Bradley,Riley, and B & W.

After pulverization, optionally additional milling and classifying iseffected by passing the twice pulverized kaolin through an airclassifying mill which contains an impact rotor for attriting the twicepulverized kaolin and an integral vane rotor classifier for classifyingthe attrited material and recycling particles that exceed a desiredsize, which may vary depending upon the application of the resultantkaolin product produced in accordance with the present invention. Forexample, twice pulverized kaolin particles that are larger than about 40microns may be removed from the kaolin being processed. The impact rotorcan be provided with bars at which the twice pulverized kaolin isimpacted. Oversized twice pulverized kaolin rejects from the airclassifier mill may be separated in a cyclone separator, and returned tothe air classifier mill for further milling or subjected to additionalgrinding and/or pulverizing.

An exemplary air classifying mill is the Mikro ACM pulverizer. In thismill, the twice pulverized kaolin is advanced by a screw conveyer andfirst impacts at the pins of the pin rotor. Particles are entrained byan air stream which enters below the pin rotor and are carried upbetween the inner wall and the shroud ring with baffles which decreaseair swirl. Particles are then deflected inward by an air dispersing ringto a vane rotor classifier. The rotor is separately driven through aspeed control which may be adjusted independently of the pin rotorspeed. Acceptable particles pass upward through the exhaust and to acollector. Oversize particles are carried downward by the internalcirculating air stream and are returned to the pin rotor for a furtherreduction. Other Classifiers are made by the following manufacturers:Alpine, Alfa Laval/Sharples, Wemco, Krebs, EIMCO, Dorr-Oliver, Denver,and Pan-O-Matic.

After the kaolin is pulverized at least twice, it is subjected to heattreatment. When kaolin is heated, it undergoes a series ofcharacteristic changes, detectable by various methods includingdifferential thermal analysis (DTA). Heat treatment may be employed toform one or more of metakaolin, partially calcined kaolin, and calcinedkaolin, depending on the temperatrure/duration of the heat treatment.Heat treatment is performed under one of an inert atmosphere, anoxidizing atmosphere, and a reducing atmosphere.

For example, after heating from about 450 to about 650° C. for asufficient period of time, kaolin undergoes a strongly endothermicdehydration reaction resulting in the starting of conversion to materialknown as metakaolin. The metakaolin state is conveniently ascertained byacid solubility testing because the alumina in the clay is virtuallycompletely soluble in strong mineral acid.

Calcining destroys the crystallinity of hydrous kaolin and renders thekaolin substantially amorphous. Calcination occurs after heating attemperatures in the range from about 700 to about 1200° C. for asufficient period of time. Commercial vertical and horizontal rotarycalciners can be used to produce metakaolin, partially calcined kaolin,and/or calcined kaolin. Operation is controlled to avoid calcining atsufficiently high temperatures to form unwanted mullite (3Al₂O₃.SiO₂).

In one embodiment, the at least twice pulverized kaolin is heated to atemperature from about 450 to about 1200° C. for a time from about 1minute to about 10 hours. In another embodiment, the at least twicepulverized kaolin is heated to a temperature from about 500 to about1100° C. for a time from about 10 minutes to about 5 hours. In aspecific embodiment, the at least twice pulverized kaolin is heated to atemperature from about 475 to about 700° C. for a time from about 5minutes to about 6 hours. In another specific embodiment, the at leasttwice pulverized kaolin is heated to a temperature from about 750 toabout 1050° C. for a time from about 15 minutes to about 4 hours.

After heat treatment, again optionally additional milling andclassifying is effected by passing the heat treated kaolin through anair classifying mill which contains an impact rotor for attriting theheat treated kaolin and an integral vane rotor classifier forclassifying the attrited material and recycling particles that exceed adesired size, which may vary depending upon the application of theresultant kaolin product produced in accordance with the presentinvention. For example, heat treated kaolin particles that are largerthan about 20 microns may be removed from the kaolin being processed.The impact rotor can be provided with bars at which the heat treatedkaolin is impacted. Oversized heat treated kaolin rejects from the airclassifier mill may be separated in a cyclone separator, and returned tothe air classifier mill for further milling or subjected to additionalgrinding and/or pulverizing.

For example, after heat treatment, another pulverization/classificationact may be performed to remove particles that have a size greater thanabout 45 microns. In another embodiment, the additionalpulverization/classification act may be performed to remove particlesthat have a size greater than about 30 microns. In yet anotherembodiment, the additional pulverization/classification act may beperformed to remove particles that have a size greater than about 20microns.

Generally speaking, one or more conventional clay processing steps suchas selective flocculation, flocc/filtration, and the like, may beemployed before or after the multiple pulverizations and heat treatment.

The Chinese kaolin processed in accordance with the present inventionmay have a higher opacity than conventionally processed Chinese kaolin(not pulverized prior to heat treatment, or only one pulverization priorto heating). Also, the Chinese kaolin processed in accordance with thepresent invention may have a higher brightness at any givencalcination/heating temperature than conventionally processed Chinesekaolin at comparable calcinations temperatures. In one embodiment, theChinese kaolin processed in accordance with the present invention andcalcined produces material that has a brightness of at least about 86.In another embodiment, the Chinese kaolin processed in accordance withthe present invention and calcined produces material that has abrightness of at least about 90. In yet embodiment, the Chinese kaolinprocessed in accordance with the present invention and calcined producesmaterial that has a brightness of at least about 95. In still yetembodiment, the Chinese kaolin processed in accordance with the presentinvention and calcined produces material that has a brightness of atleast about 96. In another embodiment, the Chinese kaolin processed inaccordance with the present invention and calcined produces materialthat has a brightness of at least about 82.

The Chinese kaolin processed in accordance with the present inventionmay have a relatively high surface area compared to conventionallyprocessed Chinese kaolin. The relatively high surface area contributesto the high opacity of the resultant Chinese kaolin by increasing thelight scattering effects thereof. In one embodiment, the Chinese kaolinprocessed in accordance with the present invention has an oil absorptionof about 60 or more. In another embodiment, the Chinese kaolin processedin accordance with the present invention has an oil absorption of about80 or more. In yet another embodiment, the Chinese kaolin processed inaccordance with the present invention has an oil absorption of about 85or more. In still yet another embodiment, the Chinese kaolin processedin accordance with the present invention has an oil absorption of about90 or more. Surface area is determined using Gardner Coleman OilAbsorption Test is based on ASTM D-1483-84 which measures grams of oilabsorbed per 100 grams of kaolin.

Referring to FIG. 1, a high level diagram of various aspects of aChinese kaolin processing methodology 10 is shown. In act 12, crudeChinese kaolin is crushed, thereby facilitating transportation andstorage from the mining site. In act 14, the kaolin is processed toachieve a desired particle size. Such processing may include one or moreof grinding, crushing, delaminating, drying, standard clay beneficiationacts, and the like. Achieving the desired particle size facilitatessubsequent processing.

After a certain desired particle size of kaolin is obtained, act 16involves the first of at least two pulverization acts. Act 18 is thesecond of at least two pulverization acts. Optionally, additionalpulverization acts may be performed before the Chinese kaolin is heated.The multiple pulverization acts not only to provide Chinese kaolinhaving desired properties, but it also exposes carbon on the surface ofthe carbon rich Chinese kaolin particles.

Act 20 involves heating the at least twice pulverized kaolin to convertthe kaolin to one or more of metakaolin, partially calcined kaolin, andcalcined kaolin. Act 22 contemplates one or more procedures includespulverization, grinding, screening, packaging, and the like.

Referring to FIG. 2, a more detailed diagram of various aspects of aChinese kaolin processing methodology 30 is shown. In act 32, crudeChinese kaolin is crushed, thereby facilitating transportation andstorage from the mining site. In act 34, grinding, such as dry milling,is performed so that the kaolin has a desired size or particlesexceeding a certain size are removed. Act 36 involves delaminating thekaolin by, for example, slurry milling, to disassemble the “booklets”into “pages”. Act 38 involves screening to at least one of remove wetmilling media and remove particles that exceed a certain size. In act40, water is removed from the kaolin, for example, by spray or rotarydrying.

After drying kaolin, act 42 involves the first of at least twopulverization acts. If in act 40 water is removed from the kaolin byspray drying, agglomerates may form. Act 42 serves to break up theseagglomerates. Act 44 is the second of at least two pulverization acts.Optionally, additional pulverization acts may be performed before theChinese kaolin is heated. The multiple pulverization acts not onlyprovide Chinese kaolin having desired properties, but it also exposescarbon on the surface of the carbon rich Chinese kaolin particles.

Act 46 involves heating the at least twice pulverized kaolin to convertthe kaolin to one or more of metakaolin, partially calcined kaolin, andcalcined kaolin. Act 48 involves pulverizing the one or more ofmetakaolin, partially calcined kaolin, and calcined kaolin to achieve adesired particle size distribution. Act 50 involves packaging the one ormore of metakaolin, partially calcined kaolin, and calcined kaolinhaving the desired properties.

Referring to FIG. 3, a system 60 to process Chinese kaolin is shown. Thesystem includes one or more of a grinder 62, delaminator 64, pulverizer66, and heater 68 coupled to a tester 70 and a controller 72. Thegrinder 62 processes kaolin by providing kaolin with desired size, thedelaminator 64 breaks apart the “booklet structure” of hydrous kaolin,the pulverizer 66 also provides kaolin with desired properties and/orgets carbon with the kaolin to the surface of the kaolin particles, andthe heater 68 heats the kaolin to provide one or more of metakaolin,partially calcined kaolin, and calcined kaolin. The tester 70 can be anydevice that measures at least one parameter associated with the kaolin(such as particle size distribution, brightness, whiteness, roughness, %moisture content, % content of particular chemical, and the like) or anyparameter associated with any one of the grinder 62, delaminator 64,pulverizer 66, and heater 68 (such as the temperature with the heater 68or the work imposed in the grinder 62).

While any one of the grinder 62, delaminator 64, pulverizer 66, andheater 68 are operating, the tester 70 tests the kaolin being processed.For example, while the grinder 62, delaminator 64, or pulverizer 66 isoperating, a sample of kaolin may be withdrawn and tested to determine aparameter, such as particle size distribution. The tester 70 sends thedata generated by the testing to the controller 72, which is adapted toreceive such kaolin parameter data from the tester 70. Alternatively,the tester 70 may measure a parameter of the grinder 62, delaminator 64,pulverizer 66, and heater 68, and send data associated with theparameter to the controller.

The controller 72 analyzes such data, and based on the analysis, sends asignal to any of the grinder 62, delaminator 64, pulverizer 66, andheater 68 to either continue the process, modify the process, orterminate the process. To facilitate such analysis, a data store ormemory 74 may be coupled to the controller 72 so that the controller 72can compare data sent by the tester 70 to stored data. The controller 72may send a signal to the tester 70 to perform a test. Examples of waysin which the controller 72 can modify a process include increasing ordecreasing the temperature in the heater 68; increasing or decreasingthe work/energy required by any of the grinder 62, delaminator 64, orpulverizer 66; continue operating any of the grinder 62, delaminator 64,or pulverizer 66 to achieve a certain desired particle sizedistribution; directing a repeat of an act such as requiring a thirdpulverization act; and the like.

The following examples illustrate the present invention. Unlessotherwise indicated in the following examples and elsewhere in thespecification and claims, all parts and percentages are by weight, alltemperatures are in degrees Centigrade, and pressure is at or nearatmospheric pressure.

COMPARATIVE EXAMPLE 1

Chinese kaolin is crushed to 2-3 cm diameter rocks, dry milled to reducekaolin to −325 mesh or 44 microns powder. The powder is thendelaminated, using ceramic beads, in water with the help of a phosphatedispersant to produce particles with 94% by weight less than 2 microns.After screening, the kaolin slurry is spray dried to reduce moisture toless than 1% by weight. The spray-dried kaolin is then. The pulverizedproduct is then calcined to temperatures that may reach 1100° C. Thecalcined product is finally pulverized to grind oversize aggregatesformed during calcination. Approximate particle size of theintermediates and final products are shown below in Table 1, as well astypical physical properties in Table 2: TABLE 1 Micron, dry-milledcalcination final less than product % feed % products % 50 99.5 98.7101.6 10 52.5 99.9 99.4 5 39 98.7 97.4 2 26.3 93.3 87.6 1 20.4 78.8 69.10.5 14.8 55.6 34.2 0.3 10 37.8 12.9 0.2 7.4 27.1 7.1

TABLE 2 total acid % carbon solubility surface area Sample (avg. of 2)(TAS) Brightness g/m² Calcination 2.16 NA NA NA Feed Calcination 0.01412.26 95.5 14.86 Product

EXAMPLE 1

Chinese kaolin is crushed to 2-3 cm diameter rocks, dry milled to reducekaolin to −325 mesh or 44 microns powder. The powder is thendelaminated, using ceramic beads, in water with the help of a phosphatedispersant to produce particles with 94% by weight less than 2 microns.After screening, the kaolin slurry is spray dried to reduce moisture toless than 1% by weight. The spray-dried kaolin is then pulverized twice(passed through two pulverizers). The twice-pulverized product is thencalcined to temperatures that may reach 975° C. The calcined product ispulverized again to grind oversize aggregates formed during calcination.Selected physical properties of the product are shown in Table 3 (suchas particle size distribution average, brightness, and the oilabsorption values): TABLE 3 size Example 1 <2 microns 85% by wt. <1micron 69% by wt. <0.5 microns 43% by wt. Brightness 95 PSD ave. 0.58microns oil absorption 95.5

EXAMPLE 2

Chinese kaolin is crushed to 2-3 cm diameter rocks, dry milled to reducekaolin to −325 mesh or 44 microns powder. The powder is thendelaminated, using ceramic beads, in water with the help of a phosphatedispersant to produce particles with 94% by weight less than 2 microns.After screening, the kaolin slurry is spray dried to reduce moisture toless than 1% by weight. The spray-dried kaolin is then pulverized twice(either passed through two pulverizers or passed twice through onepulverizer). The twice-pulverized product is then calcined totemperatures that may reach 920 to 975° C. The product has a brightnessof about 96. The calcined product is pulverized again to grind oversizeaggregates formed during calcination. Selected physical properties ofthe product are shown in Table 4 (such as particle size distributionaverage, brightness, and the oil absorption values): TABLE 4 sizeExample 2 <2 microns 85% by wt. <1 micron 66% by wt. <0.5 microns 32% bywt. Brightness 96 PSD ave. 0.68 microns oil absorption 96.2

EXAMPLE 3

Products of Comparative Example 1 and Examples 1 and 2 are evaluated ina PVC 55 (Pigment Volume Concentration, 55% by weight pigment in paint)paint evaluation. Paint testing is commonly used to compare the hidingpower (opacity) and other important properties such as whiteness,yellowness, and gloss. The properties of each paint Chinese kaolinmixture are reported in Table 5. TABLE 5 Paint Property Com. Ex. 1Example 1 Example 2 Viscosity KU @ 77° F.: 104 104 104 pH: 8.7 8.3 8.3C. Ratio 1.5 mills: 91.7 93.4 93.4 C. Ratio 3 mils: 96.9 97.9 98.1Reflectance: 91.6 92.2 92.1 Whiteness: 87.3 87.7 87.7 Yellowness: 1.71.9 1.8 Hunter L: 97.1 97.4 97.3 Hunter a: −0.8 −0.6 −0.6 Hunter b: 1.21.3 1.2 Gloss @ 60 deg: 2.3 2.2 2.2 Sheen @ 85 deg: 5.9 5.9 5.2 TintStrength: 51.2 53.9 53.9

EXAMPLE 4

Chinese kaolin is crushed to 2-3 cm diameter rocks, dry milled to reducekaolin to −325 mesh or 44 microns powder. The powder is thendelaminated, using ceramic beads, in water with the help of a phosphatedispersant to produce particles with 94% by weight less than 2 microns.After screening, the kaolin slurry is spray dried to reduce moisture toless than 1% by weight. The spray-dried kaolin is then pulverized twice(either passed through two pulverizers or one pulverizer twice). Thetwice-pulverized product is then calcined to temperatures that may reach815 to 900° F. The products have a brightness of about 92. The calcinedproduct is pulverized again to grind oversize aggregates formed duringcalcination. Selected physical properties of the product are shown inTable 6 (such as particle size distribution average, brightness, and theoil absorption values): TABLE 6 size Example 4 <2 microns 86% by wt. pH5.9 Brightness 92 PSD ave. 0.68 microns oil absorption 74

EXAMPLE 5

Product of Example 4 is evaluated in a PVC 66 (Pigment VolumeConcentration, 66% by weight pigment in paint) paint evaluation. Painttesting is commonly used to compare the hiding power (opacity) and otherimportant properties such as whiteness, yellowness, and gloss. In thistesting, the Chinese kaolin is evaluated against Georgia (USA) kaolin,Satintone® 5 HB available from Engelhard Corporation. Conventionalwisdom dictates that USA kaolin is superior in coating performance tokaolin from anywhere else in the world. The properties of each paintkaolin mixture are reported in Table 7. TABLE 7 PVC66 Satintone ® 5 HBProperty Example 4 USA Kaolin Viscosity KU @ 77° F.: 100 91 pH: 8.8 9.0C. Ratio 1.5 mills: 93.9 94.3 C. Ratio 3 mils: 98.5 98.4 Reflectance:92.0 92.0 Whiteness: 87.6 86.2 Yellowness: 1.9 2.6 Hunter L: 97.3 97.5Hunter a: −0.5 −0.8 Hunter b: 1.2 1.7 Gloss @ 60 deg: 2.3 2.5 Sheen @ 85deg: 6.5 13.0 Tint Strength: 53.4 53.6

EXAMPLE 6

Chinese kaolin is crushed to 2-3 cm diameter rocks, dry milled to reducekaolin to −325 mesh or 44 microns powder. The powder is thendelaminated, using ceramic beads, in water with the help of a phosphatedispersant to produce particles with 94% by weight less than 2 microns.After screening, the Chinese kaolin is fractionated to provide kaolinwhere 90% by weight has an average particle size diameter of 1 micron orless. After fractionation, the sample is spray dried and pulverizedeither 3, 5, or 7 times. The pulverized samples are calcined at 1982° C.for one hour and pulverized twice again to provide the final products.

Referring to FIG. 4, a graphical illustration of the beneficial effectthat multiple pre-heating pulverization acts have on scattering (blackglass scattering) is shown. The graph indicates that improved and higherscattering is achieved by increasing the number of pre-heatingpulverization acts. Higher scattering corresponds to higher opacity.

Black glass scattering is described in Kaliski, A., TAPPI, Vol. 53, No.11, November 1970, pages 2077-2084 titled “Performance of Some Clays inStarch Containing Paper-Coating Films; Part I. Black Glass Plates asModel Substrates”. Generally speaking, black glass scattering isconducted by coating a kaolin slurry containing 30% solids, by weightonto a black glass plate at a coat weight of 2-6 g/m² (expressed as drypigment). The reflectance values of the coatings after air drying ismeasured at a wavelength of 457 nm by means of an Elrepho reflectometer.The reflectance values are converted by the use of Kubelka-Munkequations to light scattering coefficients (m²/g). The light scatteringcoefficients give an indication of the opacifying potential of thekaolin. The higher the values of light scattering coefficients, therarer is the light passing through the kaolin coating or the larger isthe reflected and back scattered light. Apparently, the wavelength of457 nm corresponds to the wavelength used in the TAPPI brightness andopacity test method.

While the invention has been explained in relation to certainembodiments, it is to be understood that various modifications thereofwill become apparent to those skilled in the art upon reading thespecification. Therefore, it is to be understood that the inventiondisclosed herein is intended to cover such modifications as fall withinthe scope of the appended claims.

1. A system for automated processing of Chinese kaolin, comprising apulverizer for pulverizing Chinese kaolin; a tester for testing andgenerating data of at least one parameter of the Chinese kaolin or atleast one parameter of the pulverizer, the tester coupled to thepulverizer; and a controller, operatively coupled to the pulverizer andthe tester, for controlling operation of the pulverizer based on datareceived from the tester, the controller further coupled to a memory. 2.The system of claim 1, wherein the tester comprises a device thatmeasures particle size distribution.
 3. The system of claim 1, whereinthe parameter of the Chinese kaolin comprises at least one of particlesize distribution, brightness, whiteness, roughness, percent moisturecontent, or percent content of a particular chemical.
 4. The system ofclaim 1, wherein the parameter of the Chinese kaolin comprises particlesize distribution.
 5. The system of claim 1, wherein the parameter ofthe pulverizer comprises at least one of energy input and number ofpulverization acts.
 6. The system of claim 1, further comprising agrinder operatively coupled to the tester and the controller.
 7. Thesystem of claim 1, further comprising a delaminator operatively coupledto the tester and the controller.
 8. The system of claim 1, furthercomprising a heater operatively coupled to the tester and thecontroller.
 9. The system of claim 1, wherein the controller isoperative to send a signal to the tester to perform a test.
 10. Thesystem of claim 1, wherein the controller is operative to send a signalto the pulverizer to perform an additional pulverization act.
 11. Thesystem of claim 1, wherein the memory comprises stored data that can becompared to data generated by the tester.
 12. A system for automatedprocessing of Chinese kaolin, comprising a pulverizer for pulverizingChinese kaolin, the Chinese kaolin having a higher carbon content, alower iron oxide content, and a higher propensity to release aluminaupon heating compared to Middle Georgia (U.S.A.) kaolin; a tester fortesting and generating data of at least one parameter of the Chinesekaolin or at least one parameter of the pulverizer, the tester coupledto the pulverizer; and a controller, operatively coupled to thepulverizer and the tester, for controlling operation of the pulverizerbased on data received from the tester, the controller further coupledto a memory.
 13. The system of claim 12, wherein the tester comprises adevice that measures particle size distribution.
 14. The system of claim12, wherein the parameter of the Chinese kaolin comprises at least oneof particle size distribution, brightness, whiteness, roughness, percentmoisture content, or percent content of a particular chemical.
 15. Thesystem of claim 12, wherein the parameter of the Chinese kaolincomprises particle size distribution.
 16. The system of claim 12,wherein the parameter of the pulverizer comprises at least one of energyinput and number of pulverization acts.
 17. The system of claim 12,further comprising at least one of a grinder, delaminator, and heateroperatively coupled to the tester and the controller.
 18. The system ofclaim 12, wherein the parameter of the Chinese kaolin comprises carboncontent.
 19. The system of claim 12, wherein the controller is operativeto send a signal to the pulverizer to perform an additionalpulverization act.
 20. The system of claim 12, wherein the memorycomprises stored data that can be compared to data generated by thetester.